CN206828435U - Sargassum protein extraction system - Google Patents

Sargassum protein extraction system Download PDF

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Publication number
CN206828435U
CN206828435U CN201720254893.1U CN201720254893U CN206828435U CN 206828435 U CN206828435 U CN 206828435U CN 201720254893 U CN201720254893 U CN 201720254893U CN 206828435 U CN206828435 U CN 206828435U
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China
Prior art keywords
reactor
tank
centrifugal pan
transfer tank
negative
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Expired - Fee Related
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CN201720254893.1U
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Chinese (zh)
Inventor
马健
张志彬
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Individual
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Individual
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Abstract

A kind of Sargassum protein extraction system, including:Reducing mechanism;Powder under vacuum device for suction material, powder under vacuum device for suction material include transfer tank, the first negative pressure pump are provided with the top of transfer tank, offer drainage conduit in the bottom of transfer tank, movable suction tube is provided with transfer tank;Reaction unit, reaction unit include reactor and centrifugal pan, and reactor is set at equal intervals around the centre of form of centrifugal pan;Negative-pressure liquid suction device, negative-pressure liquid suction device include loading tank, and the second negative pressure pump is provided with tank in loading, and load and are provided with movable pipette on tank.The system is crushed to lyophilized marine alga using reducing mechanism and the decomposition of cellulase is carried out using reaction unit, and reactor supernatant is extracted by the way of centrifugation is extracted afterwards.The system realizes the Fully-mechanized protein extraction of marine alga, higher suitable for industrial production, its protein extracting ratio.

Description

Sargassum protein extraction system
Technical field
Protein Extraction equipment technical field is the utility model is related to, more specifically, more particularly to a kind of Sargassum protein Extraction system.
Background technology
The vitamin such as the mineral matters such as seaweeds are rich in iodine, potassium, calcium, magnesium, zinc, selenium and carrotene Vb, is described as natural health Food.In China, marine alga has long edible history, and modern study shows, marine algae extract have hypoglycemic, reducing blood lipid, Anticoagulation, strengthen immunity and other effects, meanwhile, marine alga also has the multiple biological activities such as anti-oxidant, heavy metal toxin expelling, antitumor Effect.
In recent years, all taking much count of for the healthcare function of marine alga both at home and abroad, the amino acid classes in Sargassum protein are complete, than Example is appropriate, and being especially rich in has the necessary eight kinds of amino acid of the mankind, also, protein content is also sufficiently close in ideal protein The content pattern of essential amino acid, therefore, sea urchin protein have very high value.
However, in the prior art, scale operation also is carried out without the extraction for Sargassum protein, for Sargassum protein Extraction be also only limited to laboratory research.
Utility model content
(1) technical problem
So, a kind of extraction system suitable for Sargassum protein how is provided, for realizing that the industrialization of Sargassum protein carries Industry is taken as, becomes those skilled in the art's urgent problem to be solved.
(2) technical scheme
The utility model provides a kind of Sargassum protein extraction system, and for extracting Sargassum protein, the extraction system includes:
For the reducing mechanism crushed to freezing marine alga;
For the powder under vacuum device for suction material conveyed to granular material, during the powder under vacuum device for suction material includes Turn tank, the first negative pressure pump is provided with the top of the transfer tank, drainage conduit is offered in the bottom of the transfer tank, in the row Valve is provided with expects pipe, movable suction tube is provided with the transfer tank, the transfer tank passes through the movable suction Pipe is connected with the reducing mechanism technique;
Be provided with reaction unit below the powder under vacuum device for suction material, the reaction unit include reactor with And centrifugal pan, the bottom of the centrifugal pan are simultaneously provided with centrifugation motor positioned at the position of form center of the centrifugal pan, positioned at it is described from The outer rim of cartridge is provided with the reactor, and the reactor is provided with multiple, whole reactors and surrounds the centrifugation The centre of form of disk circularizes to be set at equal intervals, is provided with heating coil on the outside of the reactor, is set in the bottom of the reactor Battery is equipped with, the battery is electrically connected with the heating coil, and the heating coil includes controlling switch, described anti- Answer and closure is provided with the top of kettle;
For the negative-pressure liquid suction device absorbed to liquid, the negative-pressure liquid suction device includes loading tank, in described Load and the second negative pressure pump is provided with tank, movable pipette is provided with the loading tank, the loading tank passes through the work Dynamic formula pipette is connected with the reactor technique.
Preferably, the utility model also includes controller and temperature sensor, and the temperature sensor is arranged at institute State the outside of reactor, detected in real time for the internal temperature to reactor, the temperature sensor and the controller Signal is connected, and the controller is connected with the controlling switch signal.
Preferably, the bottom of the reactor is provided with box structure, in offering mounting groove on the centrifugal pan, in The bottom of the mounting groove is provided with the sub-buckle structure with the box structure snap fit, and the reactor is arranged at the peace Clamped in tankage and with the centrifugal pan and connected by the box structure and the sub-buckle structure.
(3) beneficial effect
By said structure design, in Sargassum protein extraction system provided by the utility model, using reducing mechanism pair Lyophilized marine alga is crushed, and the decomposition of cellulase is carried out after acquisition marine algae powder using reaction unit, afterwards again using centrifugation The mode of separation obtains supernatant, and reactor supernatant is extracted, it becomes possible to obtains the higher Sargassum protein extraction of concentration Liquid.In links, the utility model using powder under vacuum device for suction material and negative-pressure liquid suction device to powder material and Liquid material carries out mechanization conveying, is so achieved that the Fully-mechanized protein extraction of marine alga, and the utility model is applied to work Industry produces, and its protein extracting ratio is higher.
Brief description of the drawings
Fig. 1 is the structure schematic diagram of Sargassum protein extraction system in the utility model embodiment;
In Fig. 1, the corresponding relation of component names and accompanying drawing number is:
Reducing mechanism 1, transfer tank 2, drainage conduit 3, movable suction tube 4, reactor 5, centrifugal pan 6, centrifugation motor 7, dress Carry tank 8, movable pipette 9.
Embodiment
Embodiment of the present utility model is described in further detail with reference to the accompanying drawings and examples.Following examples For illustrating the utility model, but can not be used for limiting the scope of the utility model.
In description of the present utility model, unless otherwise indicated, " multiple " are meant that two or more;Term " The orientation or position pass of the instructions such as interior ", " outside ", " front end in upper ", " under ", " left side ", " right side ", " ", " rear end ", " head ", " afterbody " It is to be described based on orientation shown in the drawings or position relationship, to be for only for ease of description the utility model and simplifying, rather than Indicate or imply that signified device or element there must be specific orientation, with specific azimuth configuration and operation, therefore can not It is interpreted as to limitation of the present utility model.In addition, term " first ", " second ", " the 3rd " etc. are only used for describing purpose, and can not It is interpreted as indicating or implying relative importance.
, it is necessary to illustrate in description of the present utility model, unless otherwise clearly defined and limited, term " phase Even ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected, or be integrally connected;Can To be mechanical connection or electrical connection;Can be joined directly together, can also be indirectly connected by intermediary.For this For the those of ordinary skill in field, concrete meaning of the above-mentioned term in the utility model can be understood with concrete condition.
Fig. 1 is refer to, Fig. 1 is the structure schematic diagram of Sargassum protein extraction system in the utility model embodiment.
The utility model provides a kind of Sargassum protein extraction system, and for extracting Sargassum protein, the system specifically includes:
1st, for the reducing mechanism crushed to freezing marine alga, in the utility model, reducing mechanism 1 is using trickle super Sonic disintegration device, reducing mechanism 1 include a pulverizing chamber, lyophilized marine alga are put into pulverizing chamber, can be crushed Into marine algae powder.
2nd, powder under vacuum device for suction material, in order to be conveyed to marine algae powder, the utility model, which additionally provides, to be used for The powder under vacuum device for suction material conveyed to granular material, powder under vacuum device for suction material include transfer tank 2, transfer tank 2 Top is provided with the first negative pressure pump, by, into negative pressure state, being provided with the first negative pressure pump transfer tank 2 on transfer tank 2 Movable suction tube 4.In actual production operation, after reducing mechanism 1 crushes lyophilized marine alga, manually by movable suction tube 4 It is inserted into pulverizing chamber, opens the first negative pressure pump, it becomes possible to which marine algae powder is absorbed in transfer tank 2.
Drainage conduit 3 is offered in the bottom of transfer tank 2, in being provided with valve in drainage conduit 3, after opening valve, transfer tank 2 Interior marine algae powder can export transfer tank 2 under gravity.
3rd, reaction unit, is provided with reaction unit below powder under vacuum device for suction material, and reaction unit includes reaction Kettle 5 and centrifugal pan 6, the bottom of centrifugal pan 6 and the position of form center positioned at centrifugal pan 6 are provided with centrifugation motor 7, positioned at centrifugation The outer rim of disk 6 is provided with reactor 5, and reactor 5 is provided with multiple, whole reactors and circularized around the centre of form of centrifugal pan 6 Set at equal intervals, the outside of reactor 5 is provided with heating coil, the bottom of reactor 5 is provided with battery, battery is with adding Heat coil is electrically connected, and heating coil includes controlling switch, and the top of reactor 5 is provided with closure.
Reactor 5 is an autonomous device, and it includes stainless steel casing, is internally provided with stainless steel casing by stainless Reative cell made of steel, one battery is set in the bottom of reative cell, outside in reative cell sets heating coil, heater wire Circle includes controlling switch, and heating coil is electrically connected by controlling switch and battery.Controlling switch is opened, battery can Electric energy is provided to heating coil, heating coil converts electrical energy into heat energy and reative cell is heated.
In an embodiment of the present utility model, a temperature sensor can also be set in the outside of reative cell, The temperature in reative cell is detected in real time using temperature sensor.In order to realize it is of the present utility model automatically control, this reality A controller is additionally provided with new, controller is connected with temperature sensor and controlling switch signal, by temperature sensor Reative cell internal temperature is detected in real time, controller carries out data analysis after receiving detection signal, and according to analysis result to control Switch processed is controlled, so as to realize the temperature control of reactor 5.
In order to accelerate the crushing efficiency of alginic cell wall, by marine algae powder and distilled water according to solid-liquid ratio 0.7: 1.0 Ratio is added in reactor 5, is then added sodium hydroxide and is adjusted liquid pH value to 10-11, adds cellulase afterwards, control Reaction temperature processed is at 45-55 DEG C, and the reaction time is in 40-55 minutes.
After the completion of above-mentioned operation program, centrifugally operated, its centrifugally operated are carried out to reactor 5 by centrifugal pan 6 Mode is:The rotary speed of centrifugal pan 6 is controlled at 4500-5500 rpms, 10 minutes centrifugal operations are carried out to reactor 5.
4th, for the negative-pressure liquid suction device absorbed to liquid, negative-pressure liquid suction device, which includes, loads tank 8, in loading tank The second negative pressure pump is provided with 8, loads and movable pipette 9 is provided with tank 8, loading tank 8 is by movable pipette 9 and instead The technique of kettle 5 is answered to be connected.The supernatant of reactor 5 is extracted using movable pipette 9, it becomes possible to obtain Sargassum protein.
It is right using reducing mechanism 1 in Sargassum protein extraction system provided by the utility model by said structure design Lyophilized marine alga is crushed, and the decomposition of cellulase is carried out after acquisition marine algae powder using reaction unit, afterwards again using centrifugation The mode of extraction is extracted to the supernatant of reactor 5, it becomes possible to the higher Sargassum protein extract solution of concentration is obtained, in each ring In section, the utility model is entered using powder under vacuum device for suction material and negative-pressure liquid suction device to powder material and liquid material again Row mechanization conveys, and is so achieved that the Fully-mechanized protein extraction of marine alga, and the utility model is applied to industrial production, its egg White recovery rate is higher.
Specifically, the bottom of reactor 5 is provided with box structure, in offering mounting groove on centrifugal pan 6, in mounting groove Bottom be provided with sub-buckle structure with box structure snap fit, reactor 5 is arranged in mounting groove and by box structure And sub-buckle structure is clamped with centrifugal pan 6 and connected.Reactor 5 is connected between centrifugal pan 6 using clamping mode, and it is not only installed Reliably, and convenient disassembly.
Embodiment of the present utility model in order to example and description for the sake of and provide, and be not exhaustively or will The utility model is limited to disclosed form.Many modifications and variations are aobvious and easy for the ordinary skill in the art See.Selection and description embodiment are to more preferably illustrate principle and practical application of the present utility model, and make this area Those of ordinary skill it will be appreciated that the utility model so as to designing the various embodiments with various modifications suitable for special-purpose.

Claims (3)

  1. A kind of 1. Sargassum protein extraction system, for extracting Sargassum protein, it is characterised in that including:
    For the reducing mechanism (1) crushed to freezing marine alga;
    For the powder under vacuum device for suction material conveyed to granular material, the powder under vacuum device for suction material includes transfer tank (2) the first negative pressure pump, is provided with the top of the transfer tank, drainage conduit (3) is offered in the bottom of the transfer tank, in described Valve is provided with drainage conduit, movable suction tube (4) is provided with the transfer tank, the transfer tank passes through described movable Suction tube is connected with the reducing mechanism technique;
    Be provided with reaction unit below the powder under vacuum device for suction material, the reaction unit include reactor (5) with And centrifugal pan (6), the bottom of the centrifugal pan and positioned at the centrifugal pan position of form center be provided with centrifugation motor (7), be located at The outer rim of the centrifugal pan is provided with the reactor, and the reactor is provided with multiple, whole reactors and surrounds institute The centre of form for stating centrifugal pan is circularized and set at equal intervals, heating coil is provided with the outside of the reactor, in the reactor Bottom is provided with battery, and the battery is electrically connected with the heating coil, and the heating coil includes controlling switch, Closure is provided with the top of the reactor;
    For the negative-pressure liquid suction device absorbed to liquid, the negative-pressure liquid suction device, which includes, loads tank (8), in the dress Carry and the second negative pressure pump is provided with tank, movable pipette (9) is provided with the loading tank, the loading tank passes through the work Dynamic formula pipette is connected with the reactor technique.
  2. 2. Sargassum protein extraction system according to claim 1, it is characterised in that
    Also include controller and temperature sensor, the temperature sensor be arranged at the reactor outside, for pair The internal temperature of reactor is detected in real time, and the temperature sensor is connected with the controller signals, the controller with The controlling switch signal connection.
  3. 3. Sargassum protein extraction system according to claim 1, it is characterised in that
    The bottom of the reactor is provided with box structure, in offering mounting groove on the centrifugal pan, in the mounting groove Bottom be provided with sub-buckle structure with the box structure snap fit, the reactor is arranged in the mounting groove, simultaneously Clamped and connected with the centrifugal pan by the box structure and the sub-buckle structure.
CN201720254893.1U 2017-03-16 2017-03-16 Sargassum protein extraction system Expired - Fee Related CN206828435U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720254893.1U CN206828435U (en) 2017-03-16 2017-03-16 Sargassum protein extraction system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720254893.1U CN206828435U (en) 2017-03-16 2017-03-16 Sargassum protein extraction system

Publications (1)

Publication Number Publication Date
CN206828435U true CN206828435U (en) 2018-01-02

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720254893.1U Expired - Fee Related CN206828435U (en) 2017-03-16 2017-03-16 Sargassum protein extraction system

Country Status (1)

Country Link
CN (1) CN206828435U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111004710A (en) * 2019-12-25 2020-04-14 吕梁学院 Sterile plant tissue extractor based on transgenic technology

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111004710A (en) * 2019-12-25 2020-04-14 吕梁学院 Sterile plant tissue extractor based on transgenic technology
CN111004710B (en) * 2019-12-25 2023-09-12 吕梁学院 Plant tissue sterile extractor based on transgenic technology

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Granted publication date: 20180102